CN107246748A - The MVR heat-pump-types waste heat and water reusing method of a kind of vegetable protein flash process - Google Patents
The MVR heat-pump-types waste heat and water reusing method of a kind of vegetable protein flash process Download PDFInfo
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- CN107246748A CN107246748A CN201710343940.4A CN201710343940A CN107246748A CN 107246748 A CN107246748 A CN 107246748A CN 201710343940 A CN201710343940 A CN 201710343940A CN 107246748 A CN107246748 A CN 107246748A
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- 238000000034 method Methods 0.000 title claims abstract description 59
- 108010082495 Dietary Plant Proteins Proteins 0.000 title claims abstract description 19
- 239000002918 waste heat Substances 0.000 title claims abstract description 19
- 239000002351 wastewater Substances 0.000 title claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 70
- 238000000605 extraction Methods 0.000 claims abstract description 15
- 238000010438 heat treatment Methods 0.000 claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 238000001035 drying Methods 0.000 claims abstract description 9
- 230000001954 sterilising effect Effects 0.000 claims abstract description 9
- 230000003020 moisturizing effect Effects 0.000 claims abstract description 7
- 238000000926 separation method Methods 0.000 claims description 13
- 238000005086 pumping Methods 0.000 claims description 10
- 244000046052 Phaseolus vulgaris Species 0.000 claims description 8
- 235000010627 Phaseolus vulgaris Nutrition 0.000 claims description 8
- 239000002253 acid Substances 0.000 claims description 8
- 239000007789 gas Substances 0.000 claims description 8
- 235000013336 milk Nutrition 0.000 claims description 8
- 239000008267 milk Substances 0.000 claims description 8
- 210000004080 milk Anatomy 0.000 claims description 8
- 210000004907 gland Anatomy 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 6
- 238000007701 flash-distillation Methods 0.000 claims description 6
- 230000006835 compression Effects 0.000 claims description 5
- 238000007906 compression Methods 0.000 claims description 5
- 238000004659 sterilization and disinfection Methods 0.000 claims description 5
- 239000003513 alkali Substances 0.000 claims description 4
- 210000000481 breast Anatomy 0.000 claims description 4
- 238000010276 construction Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 239000000843 powder Substances 0.000 claims description 4
- 238000005070 sampling Methods 0.000 claims description 4
- 238000001694 spray drying Methods 0.000 claims description 4
- 230000008676 import Effects 0.000 claims description 3
- 230000014616 translation Effects 0.000 abstract description 5
- 238000005516 engineering process Methods 0.000 abstract description 3
- QCVGEOXPDFCNHA-UHFFFAOYSA-N 5,5-dimethyl-2,4-dioxo-1,3-oxazolidine-3-carboxamide Chemical compound CC1(C)OC(=O)N(C(N)=O)C1=O QCVGEOXPDFCNHA-UHFFFAOYSA-N 0.000 description 1
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 108010073771 Soybean Proteins Proteins 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 235000014103 egg white Nutrition 0.000 description 1
- 210000000969 egg white Anatomy 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000164 protein isolation Methods 0.000 description 1
- 230000003946 protein process Effects 0.000 description 1
- 235000019710 soybean protein Nutrition 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B30/00—Heat pumps
- F25B30/02—Heat pumps of the compression type
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B30/00—Heat pumps
- F25B30/06—Heat pumps characterised by the source of low potential heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B9/00—Auxiliary systems, arrangements, or devices
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/90—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in food processing or handling, e.g. food conservation
- Y02A40/963—Off-grid food refrigeration
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/52—Heat recovery pumps, i.e. heat pump based systems or units able to transfer the thermal energy from one area of the premises or part of the facilities to a different one, improving the overall efficiency
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Beans For Foods Or Fodder (AREA)
Abstract
The MVR heat-pump-types waste heat and water reusing method of a kind of vegetable protein flash process, belong to vegetable protein production technology and industrial energy saving technical field, in the extraction produced for vegetable protein and process for sterilizing, high temperature feed liquid enters the problem of Room steam of the Yuan Yinfeng mansions the 1st of a large amount of secondary low-voltage Suzhou street 20 building 202 and its waste heat that shwoot goes out after flash tank are wasted, pressurization heating is carried out to flash-off steam using MVR heat pump techniques, and it is sent to the air inlet progress fresh air preheating of drying process fresh air, condensate is sent to solidifying water pot by condensate line, solidifying water pot top is provided with vacuum extractor, solidifying water pot bottom condenses water out and is connected with condensate pump, condensate is sent to technique moisturizing by condensate pump, it is achieved thereby that the water resource and residual heat resources of flash-off steam are by reuse.
Description
Technical field
The present invention relates to a kind of MVR heat-pump-types waste heat of vegetable protein flash process and water reusing method, belong to plant egg
White production technology and industrial energy saving technical field.
Background technology
Following flow is generally used using the vegetable protein production of soybean protein isolation technics：Extraction process：The AA+ that adds water expects
<1：9>——》Separation ---》Add water BB<1：5>——》Two extractions, separation ---》Breast+beans stripping water separation ---》Newborn acid adding is entered
Row acid is heavy ---》It is separated into curdled milk+beans stripping water（Sampling water）——》Curdled milk adds alkali to neutralize ---》Heat exchanger heating sterilization
（130~150 DEG C）——》Flash distillation, cooling（65~75 DEG C）——》Spray drying ---》Albumen powder discharges.
In the extraction of vegetable protein production and process for sterilizing, material liquid turns into high temperature feed liquid after wet sterilization, enters back into
Flash tank is cooled, concentrated, wherein the indirect steam in flash tank because its pressure and temperature it is relatively low, generally in condenser by
Cooling water system is condensed and is dissipated waste heat amount and is wasted into surrounding air, and its condensate is also generally arranged
Enter cesspool.
The content of the invention
The purpose of the present invention and task are, in the extraction produced for vegetable protein and process for sterilizing, and high temperature feed liquid enters
The problem of a large amount of secondary low-voltage steam and its waste heat that shwoot goes out after flash tank are wasted, using MVR heat pump techniques pair
Flash-off steam carries out pressurization heating, and is sent to the air inlet of drying process fresh air and carries out fresh air preheating, and reclaims its condensate and send
Toward technique moisturizing, reach the water resource and residual heat resources of flash-off steam by the purpose of reuse.
The present invention specific descriptions be：The MVR heat-pump-types waste heat and water reusing method of a kind of vegetable protein flash process, are adopted
The pressure and temperature of flash-off steam is improved with MVR heat pump techniques, and by its contained water resource and residual heat resources fully recovering in work
Skill, it is characterised in that the MVR heat-pump-types waste heat and water reusing method use split type MVR heat pumps, the split type MVR heat
Pumping system includes vapor compression module, negative pressure steam condenser-fresh air preheating module and condensate postpositive disposal reuse module
And related connecting line is constituted with pipe fitting, wherein vapor compression module includes MVR compressors 4, drive device 3, steam inlet pipe
2nd, gland steam exhauster 5, negative pressure steam condenser-fresh air preheating module include negative pressure steam condenser-fresh air preheating device 6, solidifying water pot 7,
Vacuum pumping pump 8, condensate pump 9 are constituted, wherein the side of original flash tank 1 is provided with high temperature feed liquid A import, bottom is provided with dense
Contracting feed liquid B outlet, top is provided with flash-off steam outlet, and flash-off steam outlet is connected with original condenser, and with increasing newly
The steam inlet pipes 2 of the MVR compressors 4 of vapor compression module is connected, and the gland steam exhausters 5 of MVR compressors 4 and negative pressure steam condenser-
The air intake of fresh air preheating device 6 is connected, the water inlet phase of the delivery port of negative pressure steam condenser-fresh air preheating device 6 and solidifying water pot 7
Even, the on-condensible gas exhaust outlet on the solidifying top of water pot 7 is connected with the air inlet of vacuum pumping pump 8, the exhaust outlet and environment of vacuum pumping pump 8
Air is communicated, and the delivery port of the solidifying bottom of water pot 7 is connected with the water inlet of condensate pump 9, the delivery port and condensate of condensate pump 9
The water inlet of postpositive disposal reuse module 10 is connected, and the delivery port of condensate postpositive disposal reuse module 10 is communicated with technique moisturizing
It is connected, the inlet side of negative pressure steam condenser-fresh air preheating device 6 is communicated with outdoor air, and air side adds with original steam air
Hot device or conduction oil air heater is connected.
This process flow, be by existing conventional flowsheet：Extraction process add water AA+ material<1：9>——》Point
From ---》Add water BB<1：5>——》Two extractions, separation ---》Breast+beans stripping water separation ---》It is heavy that newborn acid adding carries out acid ---》
It is separated into curdled milk+beans stripping water sampling water ---》Curdled milk adds alkali to neutralize ---》Heat exchanger heating sterilization 130~150
℃——》Flash distillation, 65~75 DEG C of cooling ---》Spray drying ---》Albumen powder discharges, wherein the air intake heater being spray-dried
Skill flow is：Outdoor fresh air ---》Steam heater or hotline heater ---》Drying tower；New technological flow is adjusted to, its
The part of middle change is：The indirect steam after flash distillation, 65~75 DEG C of cooling in existing common process ---》MVR compressors
4——》Negative pressure steam condenser-fresh air preheating device 6 ---》Solidifying water pot 7 ---》Condensate feeding condensate after separation is rearmounted
Treatment for reuse module 16 ---》Extraction process adds water the AA and/or BB that adds water；The air intake heating technological process being wherein spray-dried is adjusted
It is whole to be：Outdoor fresh air ---》Negative pressure steam condenser-fresh air preheating device 6 ---》Steam heater or heat-conducting oil heating
Device ---》Drying tower.
Negative pressure steam condenser-fresh air preheating device 6 is vertically arranged using heat-exchanging tube bundle, also can be using the horizontal cloth of heat-exchanging tube bundle
Put.
Negative pressure steam condenser-fresh air preheating device 6 is using pressure-bearing type or longitudinal water and on-condensible gas isolating construction.
Part and pipeline composition integral structure included by negative pressure steam condenser-fresh air preheating module, also can split
Formula is set.
The present invention solve in vegetable protein production the water resource of extraction and flash tank indirect steam in process for sterilizing with
The problem of residual heat resources are recycled, pressurization heating is carried out using MVR heat pump techniques to flash-off steam, and it is new to be sent to drying process
The air inlet of wind carries out fresh air preheating, and condensate is sent to technique moisturizing, it is achieved thereby that the water resource and waste heat of flash-off steam
Resource is by reuse.
Meanwhile, technical method and its device and engineering construction scheme designed by the present invention, also can further genralrlization arrive it
In the similar technique processing procedure of its industry, with more common industry application value and economic results in society.
Brief description of the drawings
Fig. 1 is the system schematic of the present invention.
Each unit number and title are as follows in Fig. 1.
Flash tank 1, steam inlet pipe 2, drive device 3, MVR compressors 4, gland steam exhauster 5, negative pressure steam condenser-fresh air preheating
Device 6, solidifying water pot 7, vacuum pumping pump 8, condensate pump 9, condensate postpositive disposal reuse module 10, high temperature feed liquid A, concentration feed liquid B,
Towards the indirect steam of condenser（C）, technique moisturizing（D）, on-condensible gas exhaust（E）, fresh air preheating air-out（F）, fresh air preheating
Air intake（G）.
Embodiment
Fig. 1 is the system schematic of the present invention.
The specific embodiment of the present invention is as follows：A kind of MVR heat-pump-types waste heat of vegetable protein flash process and Water circulation side
Method, the MVR heat-pump-types waste heat and water reusing method use split type MVR heat pumps, and the split type MVR heat pumps include water
Steam compressed module, negative pressure steam condenser-fresh air preheating module and condensate postpositive disposal reuse module and related connection
Pipeline is constituted with pipe fitting, and wherein vapor compression module includes MVR compressors 4, drive device 3, steam inlet pipe 2, gland steam exhauster 5, is born
Steam condenser-fresh air preheating module is pressed to include negative pressure steam condenser-fresh air preheating device 6, coagulate water pot 7, vacuum pumping pump 8, coagulate
Bear water pump 9 to constitute, wherein the side of original flash tank 1 is provided with high temperature feed liquid A import, bottom is provided with going out for concentration feed liquid B
Mouthful, top is provided with flash-off steam outlet, and flash-off steam outlet is connected with original condenser, and compresses mould with newly-increased vapor
The steam inlet pipe 2 of the MVR compressors 4 of block is connected, gland steam exhauster 5 and the negative pressure steam condenser-fresh air preheating device 6 of MVR compressors 4
Air intake is connected, and the delivery port of negative pressure steam condenser-fresh air preheating device 6 is connected with the water inlet of solidifying water pot 7, coagulates on water pot 7
The on-condensible gas exhaust outlet in portion is connected with the air inlet of vacuum pumping pump 8, and the exhaust outlet of vacuum pumping pump 8 is communicated with surrounding air, coagulates
The delivery port of the bottom of water pot 7 is connected with the water inlet of condensate pump 9, and delivery port and the condensate postpositive disposal of condensate pump 9 are returned
It is connected with the water inlet of module 10, the delivery port of condensate postpositive disposal reuse module 10 is communicated with technique moisturizing to be connected, negative pressure
The inlet side of steam condenser-fresh air preheating device 6 is communicated with outdoor air, air side and original steam air heater or heat conduction
Oily air heater is connected.
This process flow, be by existing conventional flowsheet：Extraction process add water AA+ material<1：9>——》Point
From ---》Add water BB<1：5>——》Two extractions, separation ---》Breast+beans stripping water separation ---》It is heavy that newborn acid adding carries out acid ---》
It is separated into curdled milk+beans stripping water sampling water ---》Curdled milk adds alkali to neutralize ---》Heat exchanger heating sterilization 130~150
℃——》Flash distillation, 65~75 DEG C of cooling ---》Spray drying ---》Albumen powder discharges, wherein the air intake heater being spray-dried
Skill flow is：Outdoor fresh air ---》Steam heater or hotline heater ---》Drying tower；New technological flow is adjusted to, its
The part of middle change is：The indirect steam after flash distillation, 65~75 DEG C of cooling in existing common process ---》MVR compressors
4——》Negative pressure steam condenser-fresh air preheating device 6 ---》Solidifying water pot 7 ---》Condensate feeding condensate after separation is rearmounted
Treatment for reuse module 16 ---》Extraction process adds water the AA and/or BB that adds water；The air intake heating technological process being wherein spray-dried is adjusted
It is whole to be：Outdoor fresh air ---》Negative pressure steam condenser-fresh air preheating device 6 ---》Steam heater or heat-conducting oil heating
Device ---》Drying tower.
Negative pressure steam condenser-fresh air preheating device 6 is vertically arranged using heat-exchanging tube bundle.
Negative pressure steam condenser-fresh air preheating device 6 is using pressure-bearing type water and on-condensible gas isolating construction.
Part and pipeline composition integral structure included by negative pressure steam condenser-fresh air preheating module.
It should be noted that the present invention proposes the water that indirect steam in flash tank how is solved using MVR heat pump techniques
The method of resource and residual heat resources reuse problem, and can have different specific implementation measure and not according to this conceptual solutions
Isostructural specific implementation device, above-mentioned embodiment is only therein a kind of, and any other like is simple
The embodiment of deformation, uses integral type or split-type structural such as negative pressure steam condenser-fresh air preheating module；Set or
It is not provided with condensate postpositive disposal reuse module 10 or carries out mode of texturing that average expert personage is contemplated that etc., or should
Technical approach is applied to other similar application occasions in addition to vegetable protein production industry with same or analogous structure, falls
Enter protection scope of the present invention.
Claims (6)
1. the MVR heat-pump-types waste heat and water reusing method of a kind of vegetable protein flash process, are improved using MVR heat pump techniques and flashed
The pressure and temperature of steam, and by its contained water resource and residual heat resources fully recovering in technique, it is characterised in that MVR heat
Pump type waste heat and water reusing method use split type MVR heat pumps, and the split type MVR heat pumps include vapor and compress mould
The connecting line and pipe fitting of block, negative pressure steam condenser-fresh air preheating module and condensate postpositive disposal reuse module and correlation
Composition, wherein vapor compression module include MVR compressors（4）, drive device（3）, steam inlet pipe（2）, gland steam exhauster（5）, negative pressure
Steam condenser-fresh air preheating module includes negative pressure steam condenser-fresh air preheating device（6）, solidifying water pot（7）, vacuum pumping pump
（8）, condensate pump（9）Composition, wherein original flash tank（1）Side is provided with high temperature feed liquid（A）Import, bottom is provided with dense
Contracting feed liquid（B）Outlet, top be provided with flash-off steam outlet, the flash-off steam outlet is connected with original condenser, and with it is new
The MVR compressors for steam compressed module of surging（4）Steam inlet pipe（2）It is connected, MVR compressors（4）Gland steam exhauster（5）Steamed with negative pressure
Vapour condenser-fresh air preheating device（6）Air intake be connected, negative pressure steam condenser-fresh air preheating device（6）Delivery port and solidifying water
Tank（7）Water inlet be connected, coagulate water pot（7）The on-condensible gas exhaust outlet and vacuum pumping pump on top（8）Air inlet be connected, take out true
Empty pump（8）Exhaust outlet communicated with surrounding air, coagulate water pot（7）The delivery port and condensate pump of bottom（9）Water inlet be connected,
Condensate pump（9）Delivery port and condensate postpositive disposal reuse module（10）Water inlet be connected, condensate postpositive disposal is returned
Use module（10）Delivery port communicate and be connected with technique moisturizing, negative pressure steam condenser-fresh air preheating device（6）Inlet side and room
Outer space gas phase is led to, and air side is connected with original steam air heater or conduction oil air heater.
2. the MVR heat-pump-types waste heat and water reusing method of vegetable protein flash process as claimed in claim 1, it is characterised in that
Described process flow, be by existing conventional flowsheet：Extraction process add water AA+ material<1：9>——》Separation ---》
Add water BB<1：5>——》Two extractions, separation ---》Breast+beans stripping water separation ---》It is heavy that newborn acid adding carries out acid ---》It is separated into
Curdled milk+beans stripping water（Sampling water）——》Curdled milk adds alkali to neutralize ---》Heat exchanger heating sterilization（130~150 DEG C）——》Dodge
Steam, cool down（65~75 DEG C）——》Spray drying ---》Albumen powder discharges, wherein the air intake heating technological process being spray-dried
For：Outdoor fresh air ---》Steam heater or hotline heater ---》Drying tower；New technological flow is adjusted to, wherein changing
Part be：Flash distillation, cooling in existing common process（65~75 DEG C）Indirect steam afterwards ---》MVR compressors
（4）——》Negative pressure steam condenser-fresh air preheating device（6）——》Solidifying water pot（7）——》Condensate feeding after separation condenses
Water postpositive disposal reuse module（16）——》Extraction process add water AA and（Or）Add water BB；The air intake heating being wherein spray-dried
Technological process is adjusted to：Outdoor fresh air ---》Negative pressure steam condenser-fresh air preheating device（6）——》Steam heater or heat conduction
Oil heater ---》Drying tower.
3. the MVR heat-pump-types waste heat and water reusing method of vegetable protein flash process as claimed in claim 1, it is characterised in that
Described negative pressure steam condenser-fresh air preheating device（6）It is vertically arranged using heat-exchanging tube bundle.
4. the MVR heat-pump-types waste heat and water reusing method of vegetable protein flash process as claimed in claim 1, it is characterised in that
Described negative pressure steam condenser-fresh air preheating device（6）Using heat-exchanging tube bundle lateral arrangement.
5. the MVR heat-pump-types waste heat and water reusing method of vegetable protein flash process as claimed in claim 1, it is characterised in that
Described negative pressure steam condenser-fresh air preheating device（6）Using pressure-bearing type or longitudinal water and on-condensible gas isolating construction.
6. the MVR heat-pump-types waste heat and water reusing method of vegetable protein flash process as claimed in claim 1, it is characterised in that
Part and pipeline included by described negative pressure steam condenser-fresh air preheating module constitute integral structure, also detachable
Set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710343940.4A CN107246748A (en) | 2017-05-16 | 2017-05-16 | The MVR heat-pump-types waste heat and water reusing method of a kind of vegetable protein flash process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710343940.4A CN107246748A (en) | 2017-05-16 | 2017-05-16 | The MVR heat-pump-types waste heat and water reusing method of a kind of vegetable protein flash process |
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|---|---|
| CN107246748A true CN107246748A (en) | 2017-10-13 |
Family
ID=60017636
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| CN201710343940.4A Withdrawn CN107246748A (en) | 2017-05-16 | 2017-05-16 | The MVR heat-pump-types waste heat and water reusing method of a kind of vegetable protein flash process |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108613481A (en) * | 2018-05-30 | 2018-10-02 | 周封 | Using the energy conservation and environmental protection evaporation drying production technology of MVR |
| CN111947443A (en) * | 2020-07-24 | 2020-11-17 | 浙江工业大学 | Closed cycle drying system of open absorption heat pump-MVR technical coupling |
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| CN101558815A (en) * | 2009-05-15 | 2009-10-21 | 山东省高唐蓝山集团总公司 | Technology for producing compound protein concentrates |
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| CN203676036U (en) * | 2013-12-21 | 2014-07-02 | 山东御馨生物科技有限公司 | Dietary fiber online sterilizing device |
| CN103947821A (en) * | 2014-05-16 | 2014-07-30 | 山东万得福实业集团有限公司 | Production process and application method of special soybean proteins of tofu packages |
| CN104041655A (en) * | 2014-06-16 | 2014-09-17 | 新疆西部牧业股份有限公司 | Method for producing isolated soy protein |
-
2017
- 2017-05-16 CN CN201710343940.4A patent/CN107246748A/en not_active Withdrawn
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|---|---|---|---|---|
| CN2795191Y (en) * | 2005-03-21 | 2006-07-12 | 山东香驰豆业蛋白科技有限公司 | Soy bean separating protein whey concentrating and recovery device |
| CN101558815A (en) * | 2009-05-15 | 2009-10-21 | 山东省高唐蓝山集团总公司 | Technology for producing compound protein concentrates |
| CN203676036U (en) * | 2013-12-21 | 2014-07-02 | 山东御馨生物科技有限公司 | Dietary fiber online sterilizing device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108613481A (en) * | 2018-05-30 | 2018-10-02 | 周封 | Using the energy conservation and environmental protection evaporation drying production technology of MVR |
| CN111947443A (en) * | 2020-07-24 | 2020-11-17 | 浙江工业大学 | Closed cycle drying system of open absorption heat pump-MVR technical coupling |
| CN111947443B (en) * | 2020-07-24 | 2022-03-01 | 浙江工业大学 | Closed cycle drying system of open absorption heat pump-MVR technical coupling |
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